Methods and apparatuses for removal of hydrogen sulfide and carbon dioxide from biogas
US-9339760-B2 · May 17, 2016 · US
US9771287B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9771287-B2 |
| Application number | US-201214115355-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 5, 2012 |
| Priority date | May 6, 2011 |
| Publication date | Sep 26, 2017 |
| Grant date | Sep 26, 2017 |
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Installation and method for processing wastewater, comprising: a) providing wastewater for processing; b) reducing O2 content of said wastewater by unactivated aerobic digestion; c) subsequently to ‘b’, eliminating substantially all O2 from said wastewater by anaerobic digestion; d) subsequently to ‘c’, transferring said wastewater to a closed photobioreactor; and e) subsequently to ‘d’, maintaining said wastewater in said photobioreactor in conditions favorable for algal photosynthesis, thereby allowing algae to grow in said photobioreactor. A method for growing algae is also disclosed whereby time, density and flow speed are controlled. The photobioreactor may have a conduit with two proportions of different cross sections.
Opening claim text (preview).
The invention claimed is: 1. A method for processing wastewater having an organic content comprising: a) providing wastewater comprising microorganisms for processing, wherein said wastewater is selected from the group consisting of domestic sewage, commercial sewage, industrial waste and surface runoff; b) reducing O 2 content of said wastewater by unaerated aerobic digestion by said microorganisms such that the O2 content of wastewater after said unaerated aerobic digestion is not more than 2 mg/L, changing the population of microorganisms in said wastewater from more aerobic microorganisms to fewer aerobic microorganisms, and transferring said wastewater with reduced O 2 content from said unaerated aerobic digestion to anaerobic digestion; c) subsequently to ‘b’, eliminating substantially all O 2 from said wastewater by said anaerobic digestion such that the population of aerobic microorganisms in said wastewater is no longer viable by the conditions of said anaerobic digestion; d) subsequently to ‘c’, transferring said wastewater to a photobioreactor, said photobioreactor closed to prevent microorganisms from the surroundings from entering said photobioreactor; and e) subsequently to ‘d’, maintaining said wastewater in said photobioreactor in conditions favorable for algal photosynthesis, thereby allowing algae to grow in said photobioreactor to provide purified water suitable for discharge into the environment, wherein the conditions in said photobioreactor are such that the algal population is predominantly planktonic algae, wherein the wastewater is circulated in said photobioreactor, and wherein conditions of said transferring ‘d’ and/or said maintaining ‘e’ are such that subsequent to said maintaining ‘e’, the population of microorganisms from said anaerobic digestion in said wastewater is no longer viable. 2. The method of claim 1 , further comprising, prior to said reducing of O 2 content ‘b’, reducing the organic content of said wastewater by activated aerobic digestion. 3. The method of claim 1 , wherein at least one of said reducing of O 2 content by unaerated aerobic digestion ‘b’ and said eliminating of O 2 content by anaerobic digestion ‘c’ is performed in a closed vessel. 4. The method of claim 1 , further comprising recovering CO 2 gas released by said anaerobic digestion and adding said recovered CO 2 gas to wastewater in said photobioreactor. 5. The method of claim 1 , wherein said algae are native. 6. The method of claim 1 , further comprising during said maintaining said wastewater in said photobioreactor ‘e’, at least one of circulating said wastewater in said photobioreactor discontinuously and circulating said wastewater in said photobioreactor continuously. 7. The method of claim 1 , further comprising when there is insufficient sunlight to support sufficient photosynthesis, illuminating the wastewater in the photobioreactor with artificial light. 8. The method of claim 1 , wherein said photobioreactor is operated at above ambient pressure. 9. The method of claim 1 , further comprising when there is insufficient sunlight to support sufficient photosynthesis, circulating the wastewater in the photobioreactor.
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